Experimental characterization and multi-scale modeling of mixing in static mixers

被引:56
作者
Lindenberg, Christian [1 ]
Schoell, Jochen [1 ]
Vicum, Lars [1 ]
Mazzotti, Marco [1 ]
Brozio, Joerg [2 ]
机构
[1] ETH, Inst Proc Engn, CH-8092 Zurich, Switzerland
[2] Novartis Pharma AG, Pharmaceut & Analyt Dev, CH-4002 Basel, Switzerland
关键词
CFD; competitive chemical reactions; mixing; Y-mixer; Roughton mixer;
D O I
10.1016/j.ces.2008.05.026
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Mixing in static mixers is studied using a set of competitive-parallel chemical reactions and computational fluid dynamics (CFD) in a wide range of operating conditions. Two kinds of mixers, a wide angle Y-mixer and a two jet vortex mixer, referred to as Roughton mixer, are compared in terms of reaction yields and mixing times. It is found that the Roughton mixer achieves a better mixing performance compared to the Y-mixer. The effect of flow rate ratio on mixing in the Roughton mixer has been studied as well and it is shown that the mixing efficiency is not affected by the flow rate ratio. Moreover, experimental results and model predictions are in good agreement for all mixer geometries and operating conditions. CFD is used to calculate absolute mixing times based on the residence time in the segregated zone and it is shown that mixing times of less than 1 ms can be achieved in the Roughton mixer. In addition, CFD provides insight in local concentrations and reaction rates and serves as a valuable tool to improve or to scale-up mixers. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4135 / 4149
页数:15
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